Westwater Resources Provides Results From Its Definitive Feasibility Study for Battery Graphite Production Facility
Westwater Resources Inc. (NYSE American: WWR) announced the results of its Definitive Feasibility Study (DFS) for the Coosa Graphite Project in Alabama. The total capital cost for Phase I is estimated at $202 million, expected to be completed over 17 months. The facility aims to produce battery-grade graphite, crucial for lithium-ion batteries in electric vehicles. Phase I will process 8,050 metric tons of graphite concentrate per year, with projections showing positive economic viability, including a pre-tax NPV of $119 million and an IRR of 15% over 35 years.
- Capital cost for Phase I estimated at $202 million, indicating strong financial planning.
- Projected pre-tax NPV of $119 million and an IRR of 15% demonstrate strong economic viability.
- Facility to produce battery-grade graphite, aligning with increasing demand for clean energy solutions.
- Employment opportunities for over 100 individuals during operations, benefiting local community.
- None.
Study Scope Addresses Increased Customer Interest by Increasing Production Rates
WWR is an explorer and developer of US-based mineral resources essential to clean energy production in
- Define the key components of the technology providers equipment packages, as well as the other requirements of the facility.
- Support the Project’s economic evaluation and assessment which was performed by Westwater.
- Identify and assess the processes and facilities that provides the most favorable return on investment.
- Establish a budget for financing and forecasting of the Project moving forward.
The overall capital cost of Phase I of the Project is estimated to be
“This has been a high-quality effort by the Westwater team, Samuel Engineering, Dorfner Anzaplan and Harper,” said
The role of SE and the three third-party technology providers are noted below:
- Samuel Engineering – organize, coordinate, and develop the overall DFS, to interconnect the equipment designed and supplied by the three third technology providers, and provide any remaining balance of plant design and components required for a fully operational facility.
- ANZAPLAN – engineer and design of the chemical purification process, Spherical Purified Graphite (“SPG”), and sodium hydroxide recovery and wastewater treatment for the chemical purification process. The Purification process involves caustic roasting, caustic leaching, acidic leaching, and drying. SPG, an intermediate product that is later coated to make Coated Spherical Purified Graphite (“CSPG”), requires a staged milling operation consisting of size reduction (micronizing) milling and shaping (spheronizing).
- Harper – design and pricing for two (2) vertical furnaces used in the thermal purification process.
The DFS pertains to Phase I of the Project. Westwater plans to develop the Project site in two phases (Phases I and II). A plan and design for Phase II is in place at a pre-feasibility level (“PFS”), and economics are presented for both of the phases. A third phase, involving the development of the Coosa Graphite Deposit near the
PROJECT DEVELOPMENT PLAN
Phase I: Beginning in early 2023, the Project is expected to begin processing approximately 8,050 metric tons (mt) per year of graphite concentrate. Feedstock is anticipated to be supplied from outside sources until at least 2028. After processing and purification, approximately 7,500 mt of two products would be available in the following quantities:
• | CSPG: |
3,700 mt per year |
|
• | Fine Products from SPG milling: |
3,800 mt per year |
Phase II: The feedstock processing capacity of the Project is anticipated to increase to approximately 35,200 mt per year in 2024. Upon completion of Phase II, after processing and purification, approximately 32,400 mt of two products will be available in the following quantities:
• | CSPG: |
15,800 mt per year |
|
• | Fine Products from SPG milling: |
16,600 mt per year |
PROJECT LOCATION
The property for the Project is located within the
PROPRIETARY TECHNOLOGY
Westwater has been working with third-party technology providers and equipment suppliers to develop the processes for purifying graphite to
COMMUNITY BENEFITS
Construction and operation of the proposed Graphite Processing Facility is expected to result in a positive effect on the socioeconomic characteristics of the regional area. Westwater projects that the majority of beneficial effects will result from the employment of over 100 persons once the Project is in operation.
PROJECT EXECUTION SUMMARY
In the DFS, Samuel Engineering has developed a Level 2 execution schedule encompassing engineering, procurement, construction, and start-up of Phase I of the Project.
The total estimated timeframe for construction of Phase I is estimated to be 17 months, made up of the four overlapping components below:
- Detailed Design
- Procurement
- Construction
- Commissioning and Startup
ESTIMATE ACCURACY AND CONTINGENCY ANALYSIS
The estimate in the DFS has been developed to a level sufficient to assess/evaluate the Project’s concept, various development options and overall viability. After inclusion of the recommended contingency and excluding any scope changes, the capital cost estimate for Phase I is considered to have a level of accuracy in the range of -
Contingency is an allowance to cover unforeseen costs that may arise during the execution of the Project, which reside within the scope-of-work but cannot be explicitly defined or described at the time of the estimate due to lack of more detailed information. It is assumed that contingency will be spent; however, it does not cover any Project scope changes or exclusions.
Within the DFS, the contingency allowance has been assessed by considering the quality of scope definition, takeoff quantities, and pricing obtained for each major commodity of the estimate. Each component is assigned a percentage rate based on the best judgment of the project team.
In recognition of the degree of detail on which the estimate is based, a contingency of
ECONOMIC EVALUATION
The economic viability of the Project was evaluated by developing an Economic Model (“Model”). The Model was prepared on an annual basis for the project duration which includes Phase I and Phase II of the Project.
-
Phase I consists of the
Coosa plant producing 3,700 mt per year of CSPG, the subject of the DFS. - Phase II consists of an expanded plant producing 15,800 mt per year of CSPG (PFS Level estimate)
The Model incorporated the annual figures for the feed purchase, operating costs, revenues from the sale of graphite products, as well as the capital expenditures. Based on the input parameters, the Model calculates the annual pre-tax cash flows, Net-Present-Value (NPV) of the project based on
Case I: Phase I only – This case assumes the Project has a capacity of using 8,050 mt natural graphite feedstock to produce approximately 3,700 mt CSPG per year will operate for 35 years.
- Project Duration: 35 years
-
Pre-Tax NPV-8 percent:
$119 million -
IRR:
15% -
Annual
Pre-Tax Cash Flow (After the year 2025): per year$24 million -
Project
Pre-Tax Cash Flow : .$656 million
Case II: Phase I and II. The Model assumes that the capacity of plant will increase to 35,200 mt of feedstock to produce 15,800 mt per year of CSPG product. Also assumed are
- Project Duration: 35 years
-
Pre-Tax NPV-8 percent:
$767 million -
IRR:
20.5% -
Average Annual
Pre-Tax Cash Flow (After the year 2025):$129 million -
Project
Pre-Tax Cash Flow :$3.7 billion
About
Cautionary Statement Regarding Forward-Looking Statements
This news release contains forward-looking statements within the meaning of the Private Securities Litigation Reform Act of 1995. Forward-looking statements are subject to risks, uncertainties and assumptions and are identified by words such as "expects," "estimates," "projects," "anticipates," "believes," "could," “scheduled,” and other similar words. Forward looking statements include, among other things, statements concerning the construction and operation of the Company’s
(a) the Company’s ability to successfully construct and operate a commercial-scale plant capable of producing battery grade materials in quantities and on schedules consistent with the
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